Process for producing 5-trifluoromethyluracil derivatives

Abstract: A process for producing 5-trifluoromethyluracil comprising reacting 5-trifluoromethyl-5,6-dihydrouracil with alkylsulfoxide in the presence of a halogen and an acid catalyst is disclosed.

Description: The present invention relates a process for producing 5-trifluoromethyluracil, an intermediate for the preparation of 1-(2'-deoxy-β-D-erythro-pentofuranosyl)-5-trifluoromethyluracil derivatives having anti-tumor and anti-viral activities. 1-(2'-deoxy-β-D-erythro-pentofuranosyl)-5-trifluoromethyluracil derivatives (trifluorothymidine derivatives) are compounds which have long been drawing attention because of their relationships between uridine or thymidine. Since they have anti-tumor and anti-viral activities, they are important as pharmaceuticals or intermediates for producing the pharmaceuticals, so that processes for producing them have been well studied. It is well known in the field of synthetic organic chemistry in this area that the processes for producing the derivatives largely vary depending on the type of the base in the nucleoside, so that a suitable production process should be studied for each type of the bases. For example, as described in Nucleic Acids Research 12, 6827 (1984) or in Nucleosides & Nucleotides, 8, 549 (1989), bases of nucleic acids, such as uracil, fluorouracil, thymine and trifluorothymine have largely different properties because of the difference in the substituent group on 5-position. Therefore, a production process by utilizing glycosylation must be developed for each of the above-mentioned bases. Especially, 5-trifluoromethyluridine has chemical properties largely different from those of uridine and thymidine because of the influence by the trifluoromethyl group, so that 5-trifluoromethyluridine cannot be produced well by a production process analogous to the process for producing uridine or thymidine. Further, if a compound having 2'-deoxy structure in the sugar moiety is produced by a conventional process, the selectivity of α and β isomers is low, so that it is difficult to selectively obtain the necessary β isomer alone. Known processes for producing 1-(2'-deoxy-β-D-erythro-pentofuranosyl)-5-trifluoromethyluracil derivatives include: (1) A process in which the base of thymidine is exchanged with 5-trifluoromethyluracil by nucleoside-2'-deoxyribose transferase or the like (M.G. Stout et al., Methods Carbhydr. Res., 7, 19 (1976); (2) A process in which the halogen atom at 5-position of a 1-(2'-deoxy-β-D-erythro-pentofuranosyl)-5-halouracil derivative is reacted with trifluoromethylcopper (Y. Kobayashi, et al., J.C.S. Perkin Trans I, 2755 (1980)); (3) A process in which a thymidine derivative and trifluoroacetic acid are subjected to electrolysis reaction (L. Hein, et al., DE 119423 (1976)); (4) A process in which 5-trifluoromethyl-2,4-bis-trimethylsilyloxy)pyrimidine and methyl 2-deoxy-D-erhythro-pentofuranoside derivative are reacted in the presence of an acid catalyst (Japanese Laid-open PCT Application (Kohyo) No. 62-500239)); and (5) A process in which 5-trifluoromethyl-2,4-bis(trimethylsilyloxy)pyrimidine and 3,5-di-O-(p-chlorobenzoyl)-2-deoxy-α-D-erythro-pentofuranosyl chloride are reacted in the presence of zinc chloride catalyst (Japanese Laid-open Patent Application (Kokai) No. 2-289595, Heterocycles, 31, 569 (1990)). However, the above-mentioned process (1) has a drawback in that isolation of the desired product from the reaction system is difficult so that it is difficult to produce the desired product in a large scale. The process (2) has a drawback in that a reaction intermediate is very sensitive to air, so that it is difficult to set reaction conditions and the yield is low. The process (3) has a drawback in that both the yield and electric efficiency are low, and an equipment for electrolysis which can withstand trifluoroacetic acid is necessary. The process (4) has a drawback in that the desired product is obtained as a racemate which is difficult to resolve, so that isolation yield of the desired β isomer is very low. The process (5) has a drawback in that expensive 5-trifluoromethyl-2,4-bis(trimethylsilyloxy)pyrimidine is required in a large amount. Further, in this process, it is necessary to employ zinc chloride which is hygroscopic and insoluble in solvents, and so has poor ease of handling as a catalyst, so that the reproducibility of the process is low and it is difficult to carry out the process in an industrial scale. Still further, if the expensive 5-trifluoromethyl-2,4-bis(trimethylsilyloxy)pyrimidine is used in an amount smaller than the equimolar amount, the selectivity to β isomer is extremely decreased, so that the yield of the desired β isomer is largely reduced. Thus, none of the conventional processes is suited as a process for producing 1-(2'-deoxy-β-D-erythro-pentofuranosyl)-5-trifluoromethyluracil derivatives which are important as pharmaceuticals or intermediates thereof in a large scale at a low cost with certainty. Thus, an improved process for producing 1-(2'-deoxy-β-D-erythro-pentofuranosyl)-5-trifluoromethyluracil derivatives is demanded. On the other hand, trifluoromethyluracil is a compound which has been drawing attention because of the relationship between uracil or thymine that is a base of nucleic acid. Especially, processes for producing triflurothymidine derivatives which are used as anti-cancer agents or anti-viral agents because of their specific physical properties and actions, or as important intermediates for the production of pharmaceuticals such as 1-(2'-deoxy-β-D-erythro-pentofuranosyl)-5-trifluoromethyluracil derivatives, have been intensively studied. Conventional processes for producing 5-trifluoromethyluracil include: (1) A process in which 5-hydroxycarbonyluracil is reacted with SF 4 (M.P. Merite, et al., J. Pharm. Sci., 52, 508 (1963)); (2) A process in which 5-iodouracil is reacted with trifluoromethylcopper (Y. Kobayashi et al., J.C.S. Perkin I, 2755 (1980)); (3) A process in which uracil and trifluoroacetic acid are subjected to electrolysis reaction (L. Hein, D. Cech, Z. Chem., 17, 415 (1977)); (4) A process in which 5-trifluoromethyl-5,6-dihydrouracil is reacted with bromine (C. Heiderberger, et al., J. Med. Chem., 7, 1 (1964); Japanese Laid-open Patent Application (Kokai) No. 58-174371); and (5) A process in which 5-trifluoromethyl-5,6-dihydrouracil is reacted with cupric halide (Japanese Laid-open Patent Application (Kokai) No. 60-94971). However, the above-mentioned process (1) has a drawback in that dangerous SF 4 having high toxicity must be used. The process (2) has a drawback in that a reaction intermediate is very sensitive to air, so that it is difficult to set reaction conditions and the yield is low. The process (3) has a drawback in that both the yield and electric efficiency are low, and an equipment for electrolysis, which can withstand trifluoroacetic acid is necessary. The process (4) has a drawback in that more than twice the stoichiometric amount of bromine is required and the yield is low. The process (5) has a drawback in that a large amount of residue containing copper salt is generated after the reaction, so that there are problems in ease of operation and disposal of the copper salt-containing residue. Thus, none of the conventional processes for producing trifluoromethyluracil is a process by which the desired product is produced at a low cost with certainty. Thus, an improved process is demanded. Accordingly, it is the object of the present invention to provide a process for producing trifluoromethyluracil, an intermediate of the above process, by which the desired product can be produced easily at a low cost. This object has been achieved by a dehydrogenating reaction of 5-trifluoromethyl-5,6-dihydrouracil. This compound is an intermediate in the glycosylation reaction of 5-trifluoromethyl-2,4-bis(trimethylsilyloxy)pyrimidine using a copper compound as a catalyst, by using chloroform as the solvent and by carrying out the reaction in the presence of fluoride ion, surprisingly, the reaction proceeds with very high selectivity and high yield, and satisfactory results can be obtained even if stoichiometric amounts of the reactants are used, which is very advantageous from the economical viewpoint. That is, the present invention provides a process for producing 5-trifluoromethyluracil comprising the step of: (a) reacting 5-trifluoromethyl-5,6-dihydrouracil with alkylsulfoxide in the presence of a halogen and an acid catalyst to obtain 5-trifluoromethyluracil. The process according to the present invention is expressed by the following reaction equation: Each step will now be described in detail. Step (a) In this step, 5-trifluoromethyl-5,6-dihydrouracil is reacted with alkylsulfoxide in the presence of a halogen and an acid catalyst. 5-trifluoromethyl-5,6-dihydrouracil employed as a starting material in this step is a well-known compound which can be easily obtained by reacting trifluoromethacrylic acid and urea (e.g., T. Fuchigami et al., Synthesis, 766 (1984)). The alkylsulfoxide used in this step is preferably expressed by the formula R 1 SOR 2 (wherein R 1 and R 2 , the same or different, represent C 1 - C 4 alkyl), although the alkylsulfoxide which may be employed in this step is not restricted thereto. Preferred examples of the alkylsulfoxide include dimethylsulfoxide, diethylsulfoxide and the like. Alkylsulfoxide may preferably be used in an amount of not less than one equivalent, more preferably 2 to 10 equivalents, with respect to 5-trifluoromethyl-5,6-dihydrouracil. Preferred examples of the halogen which may be employed in this step include I 2 , Br 2 , ClI and the like. Among these, I 2 is best preferred. The halogen may preferably be used in an amount of 0.01 to 10 equivalents, more preferably 0.07 to 0.5 equivalents, with respect to 5-trifluoromethyl-5,6-dihydrouracil. Examples of the acid catalyst employed include organic acids such as trifluoroacetic acid, camphor sulfonic acid, p-toluenesulfonic acid and trimethylsilyl chloride; and inorganic acids such as phosphorus pentoxide, sulfuric acid and hydrochloric acid. Among these, sulfuric acid is best preferred. The acid catalyst may be used in an amount of preferably 0.01 to 1 equivalent, more preferably 0.07 to 0.5 equivalents with respect to 5-trifluoromethyl-5,6-dihydrouracil. The reaction may be carried out either in the presence or absence of a solvent. Any solvent which does not adversely affect the reaction may be employed. Specific examples of the solvent include aprotic solvents such as chloroform, benzene, toluene, 1,2-dimethoxyethane, and dimethylformamide. To carry out the reaction in the absence of a solvent or in dimethylformamide as a solvent is preferred. The reaction temperature may be from room temperature to the boiling point of the solvent, preferably 90 - 150°C. The reaction time may usually be 0.5 - 72 hours. As will be apparent from the examples described below in detail, the above-mentioned process according to the present invention can be carried out at a low cost and is excellent in ease of operation and selectivity to β isomer of the desired end product. Thus, the process according to the present invention is much superior to the conventional processes as an industrial process from the economical viewpoint, and has a technical originality. The present invention will now be described in more detail by way of examples thereof. Reference Example 1 Synthesis of 5-trifluoromethyl-5,6-dihydrouracil In 160 ml of acetic anhydride, 13.5 g of urea was suspended and 30 g of trifluoromethacrylic acid was added to the suspension. The resulting mixture was allowed to react at 100°C for 1 hour and the reaction mixture was concentrated under reduced pressure. The obtained oil was crystallized from 150 ml of water and then recrystallized from 150 ml of water to obtain 25.9 g of 5-trifluoromethyl-5,6-dihydrouracil. m.p.: 203 - 205°C Example 1 Synthesis of 5-trifluoromethyluracil In 88.7 ml of dimethylsulfoxide, 25.2 g of 5-trifluoromethyl-5,6-dihydrouracil was dissolved and 3.47 g of iodine and 0.76 ml of concentrated sulfuric acid were added to the solution to obtain a uniform solution. The obtained solution was stirred at 140°C for 6 hours, and then cooled to room temperature, followed by adding 150 g of 3% aqueous sodium sulfite solution to reduce iodine. The resulting mixture was concentrated under reduced pressure. After adding water to the residue, the residue was extracted three times with ethyl acetate. The ethyl acetate layer was concentrated and the residue was recrystallized from 100 ml of water to obtain 21.9 g (88%) of 5-trifluoromethyluracil as white needle-shaped crystals. m.p.: 239 - 241°C NMR: identical to that reported in references Example 2 Synthesis of 5-trifluoromethyluracil In 24.7 ml of dimethylformamide, 10 g of 5-trifluoromethyl-5,6-dihydrouracil is dissolved, and 12.8 g of dimethylsulfoxide, 1.4 g of iodine and 0.54 g of concentrated sulfuric acid were added to obtain a uniform solution. The obtained solution was stirred at 117°C for 9 hours. The resultant was cooled to room temperature and 70 g of 3% aqueous sodium sulfite was added to reduce iodine. The resulting mixture was concentrated under reduced pressure. Water was added to the residue and the residue was extracted three times with ethyl acetate. The ethyl acetate layer was concentrated and the residue was recrystallized from 40 ml of water to obtain 7.2 g (73%) of 5-trifluoromethyluracil in the form of white needle-shaped crystals. Example 3 Synthesis of 5-trifluoromethyluracil In 73.9 ml of dimethylsulfoxide, 25.2 g of 5-trifluoromethyl-5,6-dihydrouracil was dissolved, and 2.44 g of iodine and 0.54 ml of concentrated sulfuric acid were added to obtain a uniform solution.. The solution was stirred at 150°C for 8 hours, and the resultant was cooled to room temperature, followed by adding 120 g of 3% aqueous sodium sulfite solution to reduce iodine. The resulting solution was concentrated under reduced pressure. After adding water to the obtained residue, the residue was extracted three times with ethyl acetate. The ethyl acetate layer was dried over anhydrous sodium sulfate and the obtained residue was crystallized from chloroform, and then recrystallized from 100 ml of water to obtain 14.8 g of 5-trifluoromethyluracil in the form of white needle-shaped crystals. Example 4 Synthesis of 5-trifluoromethyluracil In 93.6 ml of dimethylsulfoxide, 17.2 g of iodine and 3.6 ml of concentrated sulfuric acid were dissolved, and 25.2 g of 5-trifluoromethyl-5,6-dihydrouracil was added to obtain a uniform solution. The solution was stirred at 140°C for 4 hours. The resulting mixture was allowed to cool to room temperature and 500 g of 3% aqueous sodium sulfite solution was added to reduce the iodine. The resultant was concentrated under reduced pressure and the obtained residue was dissolved in 150 ml of hot water. The resulting mixture was refrigerated for 2 days and the precipitated white needle-shaped crystals were collected by filtration and dried to obtain 15.1 g of 5-trifluoromethyluracil. The obtained 5-trifluoromethyluracil can than be used according to EP-B-635 517.

Claims: A process for producing 5-trifluoromethyluracil comprising reacting 5-trifluoromethyl-5,6-dihydrouracil with alkylsulfoxide in the presence of a halogen and an acid catalyst. The process according to claim 1, wherein said alkylsulfoxide is represented by the formula R 1 SOR 2 (wherein R 1 and R 2 , the same or different, represent C 1 - C 4 alkyl). The process according to claim 1, wherein said acid catalyst is selected from trifluoroacetic acid, camphor sulfonic acid, p-toluenesulfonic acid, trimethylsilane chloride, phosphorus pentoxide, sulfuric acid and hydrochloric acid. The process according to claim 1, wherein said halogen is selected from I 2 , Br 2 and ClI.

Inventors: FUKAZAWA NOBUYUKI, ISHIBASHI HIROKI, KAWAUCHI NOBUYA, OTSUKA KENGO, FUKAZAWA, NOBUYUKI, ISHIBASHI, HIROKI, KAWAUCHI, NOBUYA, OTSUKA, KENGO
Applicants: MITSUI CHEMICALS INC, MITSUI CHEMICALS, INC.
Application year: 1994
Main classification: C07D239
IPC codes: C07H19